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Basic Violet 11:1

    • Product Name: Basic Violet 11:1
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales3@liwei-chem.com
    • Manufacturer: Nanjing Color Science Co.,Ltd
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    Specifications
    HS Code 417778
    Productname Basic Violet 11:1
    Colorindexname C.I. Basic Violet 11:1
    Colorindexnumber 45110
    Casnumber 73398-89-7
    Molecularformula C28H31ClN2O3
    Molecularweight 479.02 g/mol
    Appearance Violet powder
    Physicalstate Solid
    Odor Odorless
    Ioniccharacter Cationic
    Watersolubility Soluble
    Ethanolsolubility Soluble
    Ph 4.0-6.0 (1% aqueous solution)
    Maximumabsorptionwavelength 560 nm
    Lightfastness Moderate
    Heatstability Good
    Storageconditions Store in a cool, dry, well-ventilated place away from light

    As an accredited Basic Violet 11:1 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Basic Violet 11:1 is supplied in sealed 25 kg net fiber drums with double polyethylene inner liners.
    Container Loading (20′ FCL) Basic Violet 11:1 loaded into a 20-foot FCL container, packed in sealed drums on pallets, securely strapped for ocean freight.
    Shipping Basic Violet 11:1 is typically not regulated as dangerous goods for transport. Ship in securely closed, labeled containers, protected from moisture, light, and contamination. Follow the current SDS and applicable DOT/IATA/IMDG rules, and avoid dust generation during handling.
    Storage Store Basic Violet 11:1 in a cool, dry, well-ventilated, designated chemical storage area, protected from direct sunlight, heat, and moisture. Keep containers tightly closed, clearly labeled, and segregated from strong oxidizers, acids, and food or feed. Avoid dust generation and use appropriate personal protective equipment. Maintain good housekeeping, secondary containment where required, and follow local regulations.
    Shelf Life Basic Violet 11:1 has a shelf life of about 24 months when stored cool, dry, and dark in a tightly sealed container.
    Application of Basic Violet 11:1

    In solvent-based flexographic and gravure ink systems for surface-printed packaging films, C.I. 45175:1 is typically introduced as a pre-dissolved ethanol or ethanol/n-propyl acetate concentrate because its solubility in pure hydrocarbon carriers is insufficient to maintain a stable liquid dye solution. A starting addition range of 0.5–1.5 wt% in the finished ink is normally qualified by drawdown on corona-treated polyethylene terephthalate film, with shade strength checked against a certified reference drawdown using a K-bar No. 2 coater and ISO 7724-2:2019 colour-difference measurement. The dye is most frequently combined with alcohol-soluble nitrocellulose or polyurethane resin systems at a vehicle viscosity of 18–25 s flow time measured in a 4 mm flow cup according to ISO 2431:2019. Above 1.5 wt%, bronzing and plate gumming on laser-engraved elastomer sleeves are observed on press; below 0.3 wt%, the ink loses necessary coverage without a supplementary blue-violet pigment. Because the dye contains no inorganic heavy-metal pigments, mills often document compliance with the heavy-metal migration limits of EN 71-3:2019+A1:2021 for toy-related packaging inks when requested, but this does not establish food-contact suitability under EU 10/2011.

    Why Does pH Control Dominate Stamp-Pad Ink Shelf Life?

    Open-cell foam stamp-pad inks based on water/glycerol/glycol ether are typically prepared by metering an ethanol-based concentrate of Basic Violet 11:1 into an acidic buffered base with a pH maintained between 4.0 and 5.5. At pH values above 6.0, hydroxyl ions compete with the cationic dye sites, shifting the shade toward a bluer and duller violet and increasing the rate of precipitation when anionic wetting agents or sulphonated dyestuffs are present. Long-term storage compatibility is assessed by cycling samples for 14 days at 40°C and 60% relative humidity in sealed low-density polyethylene containers; separation is quantified by filtering through a 5 µm absolute membrane and measuring optical density of the filtrate at 560–580 nm using a UV-Vis spectrophotometer. Foam absorption feed requires the finished pad ink to remain below 5 mPa·s at 25°C by rotational viscometer, otherwise the pad surface wetting deteriorates and pad life falls below the expected 10,000 impressions. For products labelled as art materials in the United States, the chronic hazard labelling criteria of ASTM D4236-94 are used, but that standard does not address functional stability or fastness.

    Anionic Topcoats Destabilise Leather Spray Dyeing

    On chromium-tanned crust leather, Basic Violet 11:1 is sprayed from an alcohol/water solution heated to 60–80°C because cold solutions produce uneven absorption and loose surface deposits on the grain layer. The dye bath for spray application is commonly prepared at 0.5–1.0 wt% dye concentration with 20–30 vol% ethanol and 5–10 vol% butyl glycol, after which the leather is dried at 40°C and conditioned to 14–16% moisture before topcoat application. The principal process conflict is the reaction between the cationic dye and anionic acrylic binders or fatliquors in the adjacent base coat; when a wet topcoat contacts uncontrolled dye, localized precipitation forms a greenish bronze film that lowers ISO 11640:2018 dry-rub fastness from a pass at 50 cycles to a failure at 10–20 cycles. A separate cationic fixation step with a low-molecular-weight cationic polymer is therefore introduced before the topcoat, and complete migration resistance is checked by cross-sectional microscopy after 24 h at 50°C. Published quantitative migration limits for this exact dye in leather are limited, so production batches are qualified against a retained reference sample rather than against absolute extraction values.

    The principal test methods referenced in the preceding scenarios are consolidated below; no method substitutes for a production-scale retained reference.

    ApplicationStandardMeasured parameter
    Solvent-based flexo/gravure inkISO 2431:2019Flow time in 4 mm cup
    Stamp-pad inkASTM D4236-94Chronic hazard labelling obligation
    Leather spray finishingISO 11640:2018Dry-rub fastness cycles
    Polystyrene/PMMAISO 4892-2:2013Xenon arc exposure stability
    Carbon paperISO 536:2019Base paper grammage

    When a solvent-borne wood stain is required to deliver a high-chroma violet on open-pored timbers such as ash and oak, Basic Violet 11:1 is usually dissolved in an ethanol/2-butoxyethanol/methyl ethyl ketone blend rather than in aromatic hydrocarbon, because aromatic carriers do not release the dye from the wood surface at acceptable drying rates. The stain is applied by air-assisted spray at a wet-film build of 15–20 µm and wiped against the grain after 30–60 s; the dye then penetrates the vessel elements, leaving the denser latewood fibres less intensely coloured. Lightfastness is the dominant constraint: on bare wood tested under ISO 105-B02:2014 xenon arc conditions, the dye shows limited blue-scale performance, and exterior joinery use requires a UV absorber and radical scavenger package that still only extends service life rather than matching inorganic oxide pigments. Published comparative weathering data for this specific colourant in exterior-grade wood coatings are limited; therefore, laminated glass and museum display applications are generally excluded from the qualification envelope.

    When Basic Violet 11:1 Is Introduced into Acrylic or Polystyrene Melt Streams

    Although the colourant is not a high-temperature organic pigment, it can be pre-dispersed at 0.05–0.3 wt% in transparent general-purpose polystyrene and poly(methyl methacrylate) compounds when the melt temperature is held below 200°C and the screw is configured for low-shear distributive mixing. On a co-rotating twin-screw extruder with an L/D ratio of 40:1, the dye concentrate is typically fed as an ethanol-wet powder or pre-dispersed in a styrene-acrylic carrier; screw speeds above 1200 rpm are avoided because viscous dissipation can push local melt temperatures beyond the shade-stability boundary, producing a yellowing of the violet hue and a decrease in transmission. Finished mouldings are not considered food-contact polymers by default; migration and overall suitability must be assessed under the relevant polymer-specific provisions of EU 10/2011 or FDA 21 CFR 178.3297 when applicable, and published data for this specific colourant in those regulatory contexts are limited. Lightfastness of the moulded parts is evaluated under ISO 4892-2:2013 Method A with a xenon arc source; typical unstabilised acrylics containing this dye show visible fading well before 200 h, whereas UV-stabilised grades can delay the shift but do not eliminate it. Production injection moulders routinely pre-dry the colourant and the polymer at 80°C for 2–4 h when ambient relative humidity exceeds 60%, because absorbed moisture promotes hydrolysis and surface splay on the moulded article.

    Carbon-Paper and Transfer-Ribbon Coating Compatibility with Paraffin/Oil Vehicles

    Wax/oil carbon-paper coatings require a dye that remains molecularly dispersed in a molten paraffin/carnauba or paraffin/microcrystalline wax matrix; Basic Violet 11:1 is introduced via an alcohol concentrate that is stripped under vacuum before the coating mass is applied to a 20–30 g/m² base paper at 10–14 g/m² dry coating weight, with grammage checked according to ISO 536:2019. The presence of residual ethanol above 0.5% by weight disrupts the wax crystal network, causing coating mottle and transfer-density variation during hot-copy impact tests conducted at 80–100°C platen temperature. Dispersion quality is monitored by drawdown of the molten coating on a Hegman gauge; particles or recrystallised dye above 15 µm are unacceptable for high-speed typewriter ribbon coating because they generate visible pinholes. The colourant does not provide the durability of carbon black in typewriter ribbon topcoats, and for re-inking applications the coating mass is frequently adjusted to a melt viscosity of 100–200 mPa·s at 100°C by the addition of paraffin wax. Published tribological data specific to this dye in typewriter or carbon-paper systems are limited, so coating line qualification is performed against a retained masterbatch rather than a published standard.

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    Certification & Compliance
    More Introduction

    Basic Violet 11:1 is the Colour Index designation for a cationic water-soluble dye supplied as a dry powder or aqueous paste. The commercial product is standardized to a supplier-defined colour strength and is commonly released for acrylic fibre dyeing, paper stock coloration, and selected water-based ink applications. Because the dye carries a cationic charge in aqueous solution, its placement in the production sequence differs from acid and disperse dyes; anionic auxiliary agents in the same bath or furnish can form insoluble complexes that reduce colour yield and block filters. Batch certificates typically report moisture content, water-insoluble matter, pH of the aqueous solution, and relative colour strength determined against a manufacturer reference by spectrophotometric measurement.

    In dyehouse preparation, the dry powder is pasted with demineralized water at 60–80 °C and stirred with a low-shear propeller until fully dissolved. Stock solutions are often prepared at 10–20 g/L active dye, depending on the received batch strength. The use of softened water is considered mandatory in package-dyeing operations; calcium and magnesium carbonates can reduce solubility and deposit on yarn packages. Stainless steel tanks are used for stock preparation because galvanized steel surfaces can react with residual acid and contaminate the solution. The dissolved stock is screened through a 25 µm mesh before entry to the dosing line to protect machine pumps and package filters. Dosing lines are rinsed with demineralized water after each batch to prevent cross-contamination from anionic products.

    Colour strength is standardized by comparing the sample solution to a manufacturer-typified reference using a UV-Vis spectrophotometer. The concentration is adjusted to give the same absorbance at the specified absorption maximum; the exact wavelength is batch-dependent and is stated on the certificate of analysis. Colour strength is expressed relative to the reference, typically in percent, and is not equivalent to chemical purity. The difference accounts for the presence of diluents, residual moisture, and salt content. For critical shade work, the solution is prepared only from the original container and used within 8 h when stored at room temperature; extended storage in daylight can reduce colour strength through photodegradation.

    What Distinguishes Basic Violet 11:1 from Other Cationic Violet Dyes in Acrylic Exhaust Dyeing?

    The choice among Basic Violet 11:1, Basic Violet 3, and Basic Violet 10 is determined by the required spectral position and the exhaustion behaviour on polyacrylonitrile. Basic Violet 11:1 is generally selected where a red-shifted violet is required on acrylic tow or top; however, the final CIELAB coordinates depend on the substrate, finish, and heat treatment history. Comparative assessment is performed with a reflectance spectrophotometer configured with D65 illumination and 10° observer geometry. Light fastness is evaluated according to ISO 105-B02:2014; the result is reported on the 1–8 scale and applies only to the tested dyeing depth. Published comparative data for this specific product are limited; a supplier reference dyeing is required to establish meaningful fastness differences.

    On conventional acrylic package dyeing machines, the liquor ratio is commonly held between 1:8 and 1:15, with a circulation rate of 4–6 L/kg·min. The bath is set at 40–50 °C, pH is adjusted to 4.5–5.5 with acetic acid/sodium acetate buffer, and the dissolved dye is injected over 10–20 min. The dyebath is then raised at 1.0–1.5 °C/min to 98 °C, held for 45–60 min, and cooled to 60 °C before sample inspection. Heating ramps above 2 °C/min can produce outer-to-inner shade imbalance because the dye strikes rapidly on the outer package layers.

    Polyacrylonitrile Exhaust Dyeing and Package Circulation Constraints

    High-density packages above 350 g/L increase flow resistance and may cause radial shade variation if the machine pump cannot maintain the required differential pressure. Production trials on vertical spindle machines at 98 °C show that initial strike is influenced more by pH and buffer concentration than by dye concentration alone. The use of anionic levelling agents in the same bath is not recommended unless compatibility tests are performed; sulfonated or carboxylated auxiliaries can precipitate the cationic dye and reduce bath stability. Package dyeing therefore requires careful control of the buffer system and the rate of temperature rise rather than simple extension of the hold time.

    On acrylic tow and top lines, water-saturated tow is passed through a dye bath containing the dissolved dye and buffer, then steam-fixed in a tunnel steamer. The dye addition point is positioned after the wetting-out section to avoid uneven initial contact. The temperature in the steamer is maintained at 100–104 °C, and the residence time is determined by tow mass and production speed. The dyed tow is then washed and finished; residual unfixed dye is extracted with water and monitored by transmission measurement in the wash line.

    When Aqueous Paste Strength Is Adjusted for Coating Formulations

    For water-based paper and ink applications, the product is diluted with demineralized water and screened through a 10 µm filter before introduction to the coating or furnish stream. In paper pulp addition, the dye is injected at the fan pump or headbox rather than at the pulper to limit retention loss and shade variation. The addition level on dry fibre is typically between 0.5 and 2.0 g/kg for deep violet shades; the exact amount is established by drainage trials and by optical measurement of the formed sheet. High shear at the fan pump assists distribution but does not replace adequate dilution.

    In tissue and packaging grades, the dye may be pre-mixed with cationic retention aids such as polyDADMAC or cationic starch. The addition sequence changes the charge balance and therefore the retention profile; a fixed addition point is required to avoid machine-direction colour drift. Laboratory beater-dyeing studies at 1.5 % consistency and 30 min circulation time provide valid comparative data only when the same furnish lot and retention sequence are used.

    For package printing with water-based flexographic inks, the dye can be combined with acrylic copolymers and polyurethane dispersions. Formulation stability is checked by accelerated storage at 40 °C for 7 days; viscosity increase or colour strength loss indicates incompatibility. High-acid-value acrylic resins can protonate the dye and reduce solubility; neutralization with ammonia or amines may be required before the dye is added.

    Thermal Fixation and Steam Processing Conditions for Polyacrylonitrile Wovens

    Continuous pad-steam processing uses a pad mangle with a nip pressure of 2–4 bar and a bath temperature below 30 °C to avoid premature fixation. The padded fabric is steamed at 102–105 °C for 20–30 min or fixed in a stenter at 150 °C for 60–90 s, depending on fabric mass and machine configuration. Excessive drying or heatsetting can migrate the dye to the fibre surface and reduce wet rubbing fastness. Rubbing fastness is assessed using ISO 105-X12:2016 with a crockmeter finger under 9 N load.

    In acrylic fabric printing, the print paste is prepared by adding the dye solution to a non-ionic guar or synthetic thickener; anionic thickeners are avoided. The printed fabric is steamed at 102 °C for 15–30 min depending on fabric weight, then washed cold to remove thickener and unfixed dye. Print paste viscosity is adjusted to the machine type, but the dye addition should occur after the thickener is fully hydrated to prevent local over-concentration and streak formation.

    How Does Hard Water and Anionic Auxiliary Chemistry Affect Dye Bath Stability?

    Hard water cations form weakly soluble carbonates with the counterions present in the dyestuff and can create visible scum at the bath surface. A total hardness value above the supplier limitation is usually corrected with polyphosphate or a compatible chelating agent; excess chelator can compete with the dye for fibre sites and alter exhaustion. The bath stability test is performed by adding the dye solution to the prepared bath at 60 °C, agitating for 15 min, and filtering through a 5 µm membrane. A rise in filtration pressure or visible residue indicates incompatibility with the auxiliary system.

    Regulatory documentation for C.I. Basic Violet 11:1 is normally supplied with a REACH safety data sheet and any substance of very high concern above 0.1 % w/w disclosed. The product is not intentionally formulated with lead, cadmium, hexavalent chromium, mercury, or polybrominated biphenyls; compliance with RoHS 2011/65/EU and its delegated directives is confirmed by supplier screening. For food-contact paper and packaging, independent verification against FDA 21 CFR 176.170 or the applicable national measure is required before commercial use. Finished textile articles sold in the European Union must meet REACH Annex XVII restrictions, but no dye-specific restriction is assumed without supplier confirmation.

    Test matrix for routine batch inspection
    Control parameterReference methodTypical equipment
    Volatile matterISO 787-2:2021Forced-air oven
    Water-soluble matterISO 787-3:2000Soxhlet extraction apparatus
    Colour strength in solutionISO 105-Z10:1997UV-Vis spectrophotometer
    Colour fastness to washingISO 105-C10:2006Launder-Ometer
    Colour fastness to lightISO 105-B02:2014Xenon-arc fadeometer
    Colour fastness to rubbingISO 105-X12:2016Crockmeter
    Commercial product forms and handling boundaries
    FormPhysical descriptionHandling boundary
    Dry powderFree-flowing cationic dyeSieve through 250 µm before use
    Aqueous pasteHigh-viscosity liquidProtect from freezing; re-homogenize before metering

    Storage stability is maintained in closed polyethylene-lined fibre drums at temperatures below 40 °C and relative humidity below 70 %. Dry powder exposed to ambient moisture can cake and reduce weigh-out accuracy; caked material is not returned to the production bin unless passed through a 250 µm sieve. Liquid grades are protected from freezing and are re-homogenized with slow agitation before metering. The product should not be stored near strong oxidizers or anionic dry blends because accidental contact can create dust-borne incompatibility and increase cleaning burden in the colour kitchen.

    Wastewater from dyeing or paper production containing Basic Violet 11:1 is treated by coagulation and adsorption because the cationic dye is readily adsorbed onto activated sludge. Visible colour can remain in the treated effluent if the dye is not fully adsorbed; discharge limits are site-specific and measured using spectrophotometric or multiple-wavelength methods. The product should not be discharged undiluted to surface water; spill control uses inert absorbent material and the collected waste is disposed of according to local regulations.

    Occupational hygiene controls include local exhaust ventilation at powder weighing stations and dust masks conforming to EN 149 for operators. The product may stain skin and clothing; protective gloves are specified by the safety data sheet and should be nitrile or rubber, not textile. Good housekeeping prevents dry powder from becoming airborne and contaminating adjacent colour lines.

    Basic Violet 11:1 is not a direct dye for unmordanted cotton; direct application to cellulosic fibres gives limited wash fastness because the cationic dye has little substantivity for the cellulose surface. Cotton substrates require cationic pre-treatment or a suitable fixing agent, and the resulting wash fastness is evaluated using ISO 105-C10:2006. For synthetic fibres other than acrylic, such as polyester, the product shows minimal absorption under aqueous exhaust conditions below 100 °C.

    Unlike solvent dyes in the same violet shade range, Basic Violet 11:1 is water-soluble and therefore unsuitable for direct dissolution in toluene, xylene, or ketone-based systems. It is also distinct from pigment dispersions; the product is a soluble dye, not a dispersed particulate. This distinction matters in ink formulation because colour strength develops at the molecular level and may be sensitive to the anion content of the resin solution.

    Replacement of Basic Violet 3 with Basic Violet 11:1 in an existing formula requires a full comparison at the same dyeing depth using the factory reflectance system. The difference is not limited to hue angle; molecular weight and charge density differences may change the response to cationic retarder concentration and buffer strength. A factorial trial with three retarder levels and three pH values is recommended, with dyed samples assessed according to ISO 105-Z10:1997 for relative colour strength and ISO 105-B02:2014 for light fastness. Without such trials, replacement can shift the final shade and reduce repeatability in production batches.